OFF-GRID ELECTROLYSIS CONTROL METHOD AND DEVICE THEREOF INDEPENDENT OF GRID

Description

CROSS-REFERENCE TO RELATED APPLICATIONS

The subject application is a continuation of PCT/CN2021/000042 filed on Mar. 15, 2021, which claims priority on Chinese Application No. CN202010287807.3 filed on Apr. 13, 2020 in China. The contents and subject matter of the PCT international application and the Chinese priority application are incorporated herein by reference.

TECHNICAL FIELD

The present invention relates to electrolysis techniques in the electrochemical field.

BACKGROUND OF THE INVENTION

Hydrogen and oxygen are both important industrial raw materials. But the hydrogen is a completely clean energy source, and it has the characteristics of high fuel value

In addition to the reforming, decomposition, and photolysis of fossil fuels, the existing hydrogen production methods include water electrolysis for hydrogen production. So far, water electrolysis hydrogen production accounts for around 4% to 5% of the world's hydrogen production and more than 95% hydrogen is obtained through the reforming of fossil fuels, and the production process will inevitably emit CO₂. The water electrolysis technology independently utilizes clean energy that can achieve zero CO₂ emissions. Hydrogen production by water electrolysis is to dissociate water molecules into hydrogen and oxygen through an electrochemical process under the action of stable direct current, which are separated out at the cathode and anode respectively. According to the different diaphragms, it can be divided into alkaline water electrolysis, proton exchange membrane water electrolysis, and solid oxide water electrolysis. However, since water electrolysis to produce hydrogen requires a large amount of electricity with stable power (voltage, current), grid power has been used as the energy source for hydrogen production.

Using fixed power supply water hydrogen production technology, several groups of electrode plates are arranged in parallel and upright in the electrolyzer, the electrolyzer is divided into several electrolytic chambers connected in series, the number of series electrodes is set according to the DC voltage value of the power supply, and then according to the power set the size of the electrolyzer, the total voltage of the electrolyzer is the sum of the voltages of each electrolytic chambers, and the total current is the same as that of each electrolytic chamber.

Although renewable energy (such as wind and solar energy) have been used for hydrogen and oxygen production in recent years, the stability of power supply is very high due to water electrolysis for hydrogen production and oxygen production, while wind and solar energy are both have the characteristics of large fluctuation, and not only the power fluctuation range is very large, but also the voltage fluctuation range is very large. The difference between minimum and maximum voltage of the source electrical energy could be as many as ten times larger. Therefore, the existing methods and technologies for hydrogen production by electrolysis of water using wind energy and solar energy still need to rely on the grid as the main power source, while wind energy or solar energy is considered to be the source electricity. As an auxiliary power source only, even in areas with better wind resources, such as areas where annual power generation reaches 1,500 hours, the availability of wind energy is around 17.1%, and the annual available sufficient sunlight is around 1,500 hours. Basically, most of the nominal hydrogen production and oxygen production schemes using new energy still rely on the grid as the main power source, which limits the way to use clean energy to produce hydrogen.

Chinese Patent Application No. 201720255416.7 outlines a single electrolyzer and multiple electrodes in parallel, and controls the number of parallel electrodes connected by a contact switch to solve the power supply fluctuation of the electrolyzer. However, the design does not consider the power characteristics of renewable energy such as wind energy and solar energy. The first reason for the change of wind and solar power is the change of voltage. Its output voltage changes rapidly, the current then changes rapidly accordingly when the wind speed or sunlight changes. The large-scale changes, the power tracking characteristics in the wind and solar energy industries are current (power) changes based on voltage changes, and different voltages correspond to different power outputs (current changes). The present invention adopts the method of automatically controlling the number of electrodes to be connected or cut out in parallel through a very large change from the input source power. The electrolytic cell can only carry a DC power supply of about 2 volts, which can only be used when the voltage fluctuation range is small (within the allowable range of the electrode voltage), and when the size of the electrolytic cell is fixed, the range of the electrolytic cell to adapt to current changes is also very limited, such as from 0.25-0.3 amp/cm², it is not suitable for renewable energy with very large power fluctuations, meanwhile the large change of the voltage and current from the source power will damage the electrolyzer. The electric power characteristics of both wind and solar energy vary with the environment they are set up in, and the changes between the high and low voltage could be as much as ten times, which is far greater than the electrode reference voltage of 2 volts (0.6-1.1). So does the current.

SUMMARY OF INVENTION

To resolve the above problems, the present invention is proposing the control method and design structure for the electrolysis, which uses a very large fluctuation range of energy as a power source, such as wind or solar energy, so it is truly independent of the grid power, while the craft of the electrolysis is the same with traditional electrolysis.

In order to achieve the designing object, the present invention adopts the following technical solutions:

Under current technology, the conventional design of the existing electrolytic cell is that the size of the electrolytic cell is based on the current of 0.25 amp/cm² to 0.3 amp/cm². Within this current range, the performance is the best. Referred to as the reference current in the present invention, that is, the preferred reference current (Ib) is between 0.25 amp/cm² to 0.3 amp/cm², 0.3 amps per cm² is referred to as the maximum reference current in the present invention, and each electrical level is 2 volts Based on the DC voltage (the allowable variation range is 0.6-1.1 times of 2 volts), in the present invention, this voltage is called the reference voltage of the electrode.

Using renewable energy as a power source, such as wind and solar energy, the electrical power from the source varies due to the environment they are in. Usually, the voltage at the minimum available power is called the cut-in voltage, and the corresponding current is called the cut-in current (Ii). The core of the present invention is setting a certain number of basic series electrodes through the lowest cut-in voltage value of wind or solar energy at first, then setting the size of the electrode according to the ratio of the minimum cut-in current value corresponding to the minimum cut-in voltage value of wind or solar energy to the reference current value. When the power of wind or solar energy increases, the voltage of the power increases and the current of the power also increases. When the voltage increases, a certain number of electrodes will be connected in series to maintain the reference voltage of about 2 volts per electrode. On the contrary, when the voltage decreases, a certain number of series electrodes will be cut out; At the maximum reference current of the cell, an electrolyzer with the same number of electrodes in series (called parallel electrolyzer) will be connected in parallel to achieve the use of renewable energy water electrolysis (hydrogen production, Oxygen production) purpose.

FIG. 1. is a schematic diagram of the arrangement structure of the electrolyzer. The electrodes of the electrolyzer are composed of basic electrodes and a different number of series electrodes. The series electrodes are arranged on one or both sides of the basic electrodes. The electrolyzer is composed of several electrolysis chambers. The basic composition of each electrolysis chamber is the same as that of the conventional electrolysis chamber. It consists of positive and negative electrodes. Different types of diaphragms can be used in the middle of the electrodes. The DC output power of wind or solar energy is used as the total power supply of the electrolyzer.

In FIG. 1, the double contacts switch (or single-contact switch) is controlled by a controller composed of PLC or other control chips. The controller connects or cuts out a certain number of series electrodes according to the changing rule of the power supply voltage. When the power supply is initially connected, the electrode voltage has not risen high enough, the switch is at the a1/b1 position, the power supply is connected to the initial number of electrode, and the series electrodes are not connected at this time. When the voltage continues to rise, the reference voltage of each electrode reaches a higher level value (such as DC 2.2 volts), the switch is automatically connected to the a2/b2 position through the controller, the additional series electrodes will be connected, and the reference voltage of each electrode will drop; the same, when the controller detects that the reference voltage is lower than a certain level of value (for example, it is set to 1.6 volts), the connected series electrodes will be cut out of several groups, to maintain the reference voltage of each electrode at a designed voltage state, such as between 1.6-2.2 volts. The newly cutting in or cutting out series electrodes can be connected in several groups or in one by one according to the power changing value. When the power continues to increase and the electrodes connected in series can no longer consume the continuously increasing input power, the current of the electrodes will reach or exceed the maximum reference current Imax (such as 0.3 amps or 0.35 amps), then connect one or more in parallel electrolyzers with the same number of electrodes in series as the basic electrolyzer is referred to in the present invention as parallel electrolyzer; also as the power continues to decrease, the current in the electrolyzer is reduced to less than the setting reference current (such as 0.2 amp/cm² or 0.1 amp/cm²), the electrolyzers connected in parallel will be automatically cut out one by one. That is, the voltage increases or decreases, the number of electrodes is connected in series or cut out first, and the current increases or decreases by connecting or cutting out the parallel electrolytic cell. When the negative electrode of the electrode is the common terminal, the negative electrode may not be set to be always in the ON state. The following will specifically illustrate how the series electrodes and the parallel electrolytic cells are connected or cut out through different embodiments.

The present invention provides a device for electrolysis comprising a power supply for supplying power to electrolysis, wherein the power supply is a fluctuating power supply with a power fluctuation in a range from a minimum power to a maximum power, and the maximum power is greater than 2 times of the minimum power, and in a range from a minimum cut-in current to a maximum current, and the maximum current is greater than 3 times of the minimum cut-in current.

In the present invention, the device may further comprise an electrolyzer system, wherein the electrolyzer system comprises a basic electrolyzer comprising a plurality of groups of basic electrodes connected in series with each other and a plurality of groups of controllable series electrodes, and a plurality of controllable parallel electrolyzers, wherein a number of the basic electrodes in the basic electrolyzer is set according to a minimum cut-in voltage value of the fluctuating power supply.

In the present invention, the reference voltage of each of the basic electrodes and the controllable series electrodes may be set to be between 1 to 2 Vdc.

In the present invention, the parallel electrolyzer may comprise the same number of the plurality of groups of basic electrodes connected in series with each other and the same number of the plurality of groups of controllable series electrodes as in the basic electrolyzer.

In the present invention, the size of the electrolyzer may be set according to the ratio of Ii/Ib, Ii is the minimum cut-in current corresponding to the minimum cut-in voltage of the fluctuating power supply, Ib is a reference current corresponding to the reference voltage, and the ratio Ii/Ib may be in a range of from 0.003 to 10.

In the present invention, the reference current Ib may be in a range of from 0.01 to 0.35 amp per square centimeter.

In the present invention, the number of the controllable parallel electrolyzers in the device may be 0 to 5, and the controllable parallel electrolyzer may be connected or cut out in parallel according to the power fluctuation.

In the present invention, the number of the controllable series electrodes may be connected or cut out in series according to the positive and negative voltage fluctuation of 20% or more, respectively.

In the present invention, the device may further comprise a controller, wherein the controller detects voltage, current, and the fluctuating power, connects with and controls that controllable series electrodes being connected in cutting in or cutting out in series and the controllable parallel electrolyzers being connected in cutting in or cutting out in parallel, and the controller comprises a negative terminal and a positive terminal, the negative terminal is a control terminal of the controller, and the positive terminal is a common terminal.

Further, the present invention provides a method for supplying and maintaining power supply for electrolysis, comprising providing a power supply for supplying power to electrolysis, wherein the power supply is a fluctuating power supply with a power fluctuation in a range from a minimum power to a maximum power, and the maximum power is greater than 2 times of the minimum power, and in a range from a minimum cut-in current to a maximum current, and the maximum current is greater than 3 times of the minimum cut-in current; providing an electrolyzer system, wherein the electrolyzer system comprises a basic electrolyzer comprising a plurality of groups of basic electrodes connected in series with each other and a plurality of groups of controllable series electrodes, and a plurality of controllable parallel electrolyzers; setting a number of the basic electrodes in the basic electrolyzer according to a minimum cut-in voltage value of the fluctuating power supply; setting a size of the basic electrolyzer and the controllable parallel electrolyzers according to a ratio of Ii/Ib, Ii is the minimum cut-in current corresponding to the minimum cut-in voltage of the fluctuating power supply, Ib is a reference current corresponding to the reference voltage, and the ratio Ii/Ib is in a range of from 0.003 to 10, and connecting in or cutting out the number of the controllable parallel electrolyzers in the device according to the power fluctuation.

In the method of the present invention, the reference voltage of each of the basic electrodes and the controllable series electrodes may be set to be between 1 to 2 Vdc.

In the method of the present invention, the parallel electrolyzer may comprise the same number of the plurality of groups of basic electrodes connected in series with each other and the same number of the plurality of groups of controllable series electrodes as in the basic electrolyzer.

In the method of the present invention, the reference current Ib may be in a range of from 0.01 to 0.35 amp/cm².

In the method of the present invention, the number of the controllable parallel electrolyzers in the device may be 0 to 5.

The method of the present invention may further comprise the steps of connecting in the controllable series electrodes according to a positive voltage fluctuation of 20% or more, and cutting out the controllable series electrodes according to a negative voltage fluctuation of 20% or more.

In the method of the present invention, the device may further comprise a controller, wherein the controller detects voltage, current, and the fluctuating power, connects with and controls that controllable series electrodes being connected in cutting in or cutting out in series and the controllable parallel electrolyzers being connected in cutting in or cutting out in parallel, and the controller comprises a negative terminal and a positive terminal, the negative terminal is the control terminal of the controller, and the positive terminal is the common terminal.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 shows the basic structure of the electrolyzer of the present invention.

FIG. 2 shows the control method of the basic electrolytic cell and the parallel electrolytic cell in the present invention.

DETAILED DESCRIPTION OF THE INVENTION

Due to the characteristics of renewable energy and customized power generation scales, the implementation of the present invention will be described in detail below with referenced examples. Defining the number of basic electrodes (electrolysis chambers) will be described in detail including the criteria of cutting-in and cutting-out of electrodes and electrolyzers. So do how to resize the electrode, and the approaches to the electrolyzers cutting in and out.

However, this should not limit the scope of protection of the present invention. It is understood that the professionals in the area can easily subdivide the number of electrodes and the number of electrolyzers in these embodiments without violating the scope of these claims. Changes and combinations, especially re-setting new reference current, reference voltage, or re-setting the minimum cut-in voltage, cut-in current, or re-setting the ratio of the minimum cut-in current and the reference current, so as to obtain a new specific implementation method, These new specific implementations obtained by changing the reference current, the reference voltage, the minimum cut-in voltage and the minimum cut-in current, the ratio setting of the minimum cut-in current and the reference current, the change of the number of electrodes, and the combination are also included in the protection scope of the present invention.

Example 1

Example 1 is a single generator using 0.25 amp as the reference current scheme. Select a wind turbine with a rated power 100 kw, the generator is a three-phase permanent magnet synchronous generator, the rated voltage of the generator is 110 Vac, the rated wind speed is 12 m/s, and the output of the generator is rectified and connected in parallel to the DC bus bar as the power supply for the electrolyzers. The following Table 1-1 shows the power output characteristics of a certain wind turbine at different wind speeds:

TABLE 1-1
Wind (m/s)	Vac	Vdc	Idc	Watt

12	110.0	146.3	683.5	100000
11.5	105.4	140.2	627.8	88014
11	100.8	134.1	574.4	77025
10.5	96.3	128.0	523.3	66992
10	91.7	121.9	474.7	57870
9.5	87.1	115.8	428.4	49617
9	82.5	109.7	384.5	42188
8.5	77.9	103.6	343.0	35540
8	73.3	97.5	303.8	29630
7.5	68.8	91.4	267.0	24414
7	64.2	85.3	232.6	19850
6.5	59.6	79.2	200.5	15893
6	55.0	73.2	170.9	12500
5.5	50.4	67.1	143.6	9628
5	45.8	61.0	118.7	7234
4.5	41.3	54.9	96.1	5273
4	36.7	48.8	75.9	3704

The basic reference current of the electrode of the electrolyzer in the example is set at 0.25 amp/cm², and the maximum reference current is 0.3 amp/cm², as shown in Table 1-2:

				Number of	size of	available
Wind	Vdc	Idc	Power	electrodes	electrode	power
(m/s)	(V)	(A)	(w)	in series	(cm2)	(w)
4	48.8	75.9	3706	26	304	3706
4.5	54.9	96.1	5277	29	304	5277
5	61	118.7	7239	32	304	7239
5.5	67.1	143.6	9635	35	304	9635
6	73.2	170.9	12509	38	304	12509
6.5	79.2	200.5	15883	41	304	15883
7	85.3	232.6	19840	44	304	19840
7.5	91.4	267.0	24404	47	304	24404
8	97.5	303.8	29620	50	304	29620
8.5	104	343.0	35530	53	304	35530
9	110	384.5	42178	56	304	42178
9.5	116	428.4	49608	59	304	49608
10	122	474.7	57862	62	304	57862
10.5	128	523.3	66986	65	304	66986
11	134	574.4	77021	68	304	77021
11.5	140	627.8	88011	71	304	88011
12	146	683.5	100000	74	304	100000
	Max.
	allowable			allows	Power
	power	Excess		power	actually	excess
	consumption	power	size of	consumption	consumed	power
	of series	of series	parallel	of parallel	by parallel	of parallel
Wind	electrodes	electrolyzers	electrolyzer	electrolyzer	electrolyzer	electrolyzer
(m/s)	(w)	(w)	1 (cm2)	1 (w)	1 (w)	1 (w)
4	4447	−741
4.5	5007	270	384	6332	270	−6062
5	5563	1676	384	7027	1676	−5352
5.5	6120	3515	384	7730	3515	−4215
6	6676	5833	384	8433	5833	−2600
6.5	7223	8660	384	9124	8660	−463
7	7779	12060	384	9827	12060	2234
7.5	8336	16068	384	10529	16068	5539
8	8892	20728	384	11232	20728	9496
8.5	9448	26081	384	11935	26081	14147
9	10005	32173	384	12637	32173	19536
9.5	10561	39047	384	13340	39047	25707
10	11117	46745	384	14043	46745	32702
10.5	11674	55312	384	14746	55312	40566
11	12230	64791	384	15448	64791	49342
11.5	12786	75225	384	16151	75225	59074
12	13343	86657	384	16854	86657	69804

The Following is connected to and continued from the above form:

	Parallel	Actual			Parallel	Actual
	electrolyzers	power	Parallel		electrolyzers	power	Parallel
Size of	2 allow	consumption	electrolyzer	Size of	3 allow	consumption	electrolyzer
parallel	power	of parallel	2 surplus	parallel	power	of parallel	3 surplus
electrolyzer	consumption	electrolyzers	power	electrolyzer	consumption	electrolyzers	power
2 (cm2)	(w)	2 (w)	(w)	3 (cm2)	(w)	3 (w)	(w)
930	23808	2234	−21574
930	25501	5539	−19962
930	27203	9496	−17707
930	28904	14147	−14758
930	30606	19536	−11070
930	32308	25707	−6602
930	34010	32702	−1308
930	35712	40566	4854	2093	80383	4854	−75528
930	37414	49342	11929	2903	116788	11929	−104859
930	39116	59074	19958	2903	122100	19958	−102142
930	40818	69804	28986	2903	127413	28986	−98427

The steps to connect the cutting in/cutting out electrodes are as follows: According to the table above, when the wind speed is 4 m/s, the power of the 100 kw turbine is 3706 watts, the rectified DC voltage is 48.8 volts, and the DC current is 75.9 amp. When the reference voltage is defined at 2-volt level, 48.8 volts can accommodate 25-26 basic electrodes in series. By following the electrode voltage changing rate, in this embodiment, 26 strings are defined at 48.8-volt level, and then according to the reference current of the electrode per square centimeter is 0.25 amps, 75.9 amps requires 304 cm² electrode (75.9/0.25), so 304 cm² is the effective size for a basic electrode (electrolyzer).

When the wind speed increased to 4.5 m/s, the DC voltage increased to 54.9 volts, with the DC current increasing to 96.1 amps, the DC power also increased to 5277 watts, 54.9 volts required 29 series electrodes, when the DC voltage is 54.9 volts, the maximum power that the series electrodes can carry is 54.9 volts×304 (electrode size)×0.3 amps (maximum reference current)=5007 watts, but the power supply 5277 watts, which is 270 watt more than the electrolyzer at 29 series electrodes. So it requires a new electrolyzer in parallel connecting (called parallel electrolyzer) to consume the additional power of 270 watts. The electrolyzer connected in parallel must has the same number of electrodes and series electrodes as the basic electrolyzer to keep the voltage of each electrode consistent, but the size of the electrolyte can be the same as the basic electrode or it also can be reset according to the new ratio of Li/Lb. This embodiment sets the effective size of the parallel electrolyzer according to the new current.

At 54.9-volt level, the DC current is 96. lamps, the electrode effective size of the parallel electrolyzer is 96.1/0.25=384 cm² (i.e, relative to the basic electrolyzer, the minimum cut-in current of the parallel electrolyzer is increased from 75.9 amps to 96.1 amps). The maximum power of an electrolyzer with 384 cm² can carry 6332 watts under the condition of 29-stage series electrodes, while the fluctuating power for the parallel electrolyzer is 270 watts (because the basic electrolyzer and the parallel electrolyzers are connected in parallel with each other, the voltage of electrolyzers are the same. The current is distributed according to the area of the electrolyzer, so the actual current of the electrolyzer is distributed in proportion to the size of the electrolyzer), so the parallel electrolyzer still has a surplus capacity of 6062 watts (in the following embodiments, the electrolyzer has a surplus capacity of 6062 watts. The calibration is a negative value. When the power is negative, there is no need to connect a new electrolyzer in parallel); when the wind speed increases to 6.5 m/s, the parallel electrolyzer still has a surplus capacity of 463 watts without requiring a new parallel electrolyzer; When the wind speed reaches 7 m/s, the voltage increases to 85.3 volts and the current increases to 232.6 amps. At this point, the output power of the turbine is greater than the basic electrolyzer and the parallel electrolyzer #1. The loadable power of 2234 watts requires a new electrolyzer #2 in parallel. The electrode size of parallel electrolyzer #2 is defined at 232.6 amps, and the size is 232.6/0.25=930.4 cm². Three electrolyzers in parallel with each other (basic electrolyzer, parallel electrolyzer #1 and parallel electrolyzer #2) are actually the power consumed that is 19,840 watts (power supply), and the three electrolyzers have a surplus capacity of 21,574 watts. When the output power of the wind turbine is greater than the power that the electrolyzer can carry, a new electrolyzer must be connected in parallel. However, the size of the electrolyzer can be the same as that of the basic electrolyzer, or it can be re-sized according to the current when the electrolyzers are connected in parallel.

Example 2

Example 2 is a single generator using 0.07 amp as the reference current scheme. Example 2 is a single generator using 0.07 amp as the reference current scheme. Example 2 uses the same wind turbine as Example 1, but the reference current is reduced to 0.07 amp/cm², and the maximum reference current is still 0.3 amp/cm², as shown in Table 2:

						Available
						power
				quntity	size of	for series
Wind	Vdc	Idc	Power	of series	electrode	electrodes
(m/s)	(V)	(A)	(w)	electrodes	(cm 2)	(w)
4	48.8	75.9	3706	26	1085	3706
4.5	54.9	96.1	5277	29	1085	5277
5	61	118.7	7239	32	1085	7239
5.5	67.1	143.6	9635	35	1085	9635
6	73.2	170.9	12509	38	1085	12509
6.5	79.2	200.5	15883	41	1085	15883
7	85.3	232.6	19840	44	1085	19840
7.5	91.4	267.0	24404	47	1085	24404
8	97.5	303.8	29620	50	1085	29620
8.5	103.6	343.0	35530	53	1085	35530
9	109.7	384.5	42178	56	1085	42178
9.5	115.8	428.4	49608	59	1085	49608
10	121.9	474.7	57862	62	1085	57862
10.5	128	523.3	66986	65	1085	66986
11	134.1	574.4	77021	68	1085	77021
11.5	140.2	627.8	88011	71	1085	88011
12	146.3	683.5	100000	74	1085	100000
	Max
	allowable
	consumption	Surplus		Parallel	Power	Surplus
	power	power		electrolyzer 1	consumption	power of
	of series	of series	quantity of	allows power	of parallel	parallel
Wind	electrodes	electrolyzers	parallel	consumption	electrolyzer	electrolyzer
(m/s)	(w)	(w)	electrolyzers	(w)	1 (w)	1 (w)
4	17631	−13925	0
4.5	19836	−14559	0
5	22040	−14801	0
5.5	24244	−14609	0
6	26448	−13939	0
6.5	28615	−12732	0
7	30819	−10979	0
7.5	33023	−8619	0
8	35227	−5608	0
8.5	37431	−1902	0
9	39635	2543	1	39635	2543	−37092
9.5	41839	7769	1	41839	7769	−34071
10	44043	13819	1	44043	13819	−30224
10.5	46247	20739	1	46247	20739	−25508
11	48451	28570	1	48451	28570	−19881
11.5	50655	37356	1	50655	37356	−13299
12	52859	47141	1	52859	47141	−5718

According to the same method as example 1, when the effective power of the wind turbine starts coming in, the DC voltage is 48.8 volts, the basic electrolyzer is provided with 26-stage series electrodes, and the reference current is reduced to 0.07 amps when the DC current is 75.9 amps, then the basic electrolyzer size is 75.9/0.07=1085 cm², no additional electrolyzer is needed if the wind speed is no higher than 9 m/s. When the wind speed is higher than 9 m/s, the output power of the wind turbine (power supply) is greater than the power that the electrolyzer can carry, and an additional electrolyzer is needed under the condition that the size of the additional electrolyzer is the same as that of the basic electrolyzer, the output power of the wind turbine can be met under the rated wind condition without adding a new electrolyzer.

Example 3

Example 3 is a single generator using 0.037 amp as the reference current scheme. Example 3 uses the same wind turbine as Example 1, but the reference current is reduced to 0.037 amp/cm², and the maximum reference current is set to 0.333 amp/cm², as shown in Table 3:

							Max
							allowable
						Available	consumed	Surplus
					size of	power	power	power
				quantity	basic	for series	of series	of series	quantity of
Wind	Vdc	Idc	power	of series	electrode	electrodes	electrodes	electroyzers	parallel
(m/s)	(V)	(A)	(w)	electrodes	(cm 2)	(w)	(w)	(w)	electrolyzers
4	48.8	75.9	3706	26	2053	3706	33356	−29650	0
4.5	54.9	96.1	5277	29	2053	5277	37532	−32255	0
5	61	118.7	7239	32	2053	7239	41703	−34464	0
5.5	67.1	143.6	9635	35	2053	9635	45873	−36238	0
6	73.2	170.9	12509	38	2053	12509	50043	−37535	0
6.5	79.2	200.5	15883	41	2053	15883	54145	−38262	0
7	85.3	232.6	19840	44	2053	19840	58315	−38475	0
7.5	91.4	267.0	24404	47	2053	24404	62486	−38081	0
8	97.5	303.8	29620	50	2053	29620	66656	−37036	0
8.5	103.6	343.0	35530	53	2053	35530	70826	−35296	0
9	109.7	384.5	42178	56	2053	42178	74996	−32818	0
9.5	115.8	428.4	49608	59	2053	49608	79167	−29559	0
10	121.9	474.7	57862	62	2053	57862	83337	−25474	0
10.5	128	523.3	66986	65	2053	66986	87507	−20521	0
11	134.1	574.4	77021	68	2053	77021	91677	−14657	0
11.5	140.2	627.8	88011	71	2053	88011	95848	−7837	0
12	146.3	683.5	100000	74	2053	100000	100018	−18	0

When the effective power of the wind turbine starts cutting in, the DC voltage is 48.8 volts, the basic electrodes are set with 26 series in the basic electrolyzer, the DC current is 75.9 amps, the reference current is reduced to 0.037 amps, the maximum reference current is 0.333 amp/cm², and the effective size of the electrode is 75.95/0.037=2053 cm², a 2053 cm² electrolyzer with 146.3 volts and 683.5 amps at maximum power, it can carry 100,018 watts with the maximum allowable reference current increased to 0.333 amp/cm², greater than the maximum power of the fluctuating power supply, the basic electrolyzer can still meet the demand without additional parallel electrolyzer. However, due to the relatively low power at low wind speed, the hydrogen and oxygen production is very small, the equipment works under low load conditions, and the effective utilization rate of the equipment is at low end.

Example 4

In Example 4, two identical generators are connected in parallel as the power supply, and 0.1 amp is used as the reference current scheme. Example 4 uses two wind turbines that are the same as example 1, after rectification and output in parallel as the power supply for the electrolyzers. The reference current is defined at 0.1 amp/cm² and the maximum reference current is 0.333 amp/cm² as shown in Table 4:

							Max
							allowable
				quantity	size of	Available	consumed
				of basic	electrode	power	power
				electrodes	in basic	for series	of series
Wind	Vdc	Idc	Power	in basic	electrolyzer	electrodes	electrodes
(m/s)	(V)	(A)	(w)	electrolyzer	(cm 2)	(w)	(w)
4	48.8	152	7412	26	1519	7412	24684
4.5	54.9	192	10554	29	1519	10554	27770
5	61	237	14477	32	1519	14477	30855
5.5	67.1	287	19270	35	1519	19270	33941
6	73.2	342	25017	38	1519	25017	37027
6.5	79.2	401	31767	41	1519	31767	40061
7	85.3	465	39680	44	1519	39680	43147
7.5	91.4	534	48808	47	1519	48808	46233
8	97.5	608	59239	50	1519	59239	49318
8.5	104	686	71059	53	1519	71059	52404
9	110	769	84356	56	1519	84356	55489
9.5	116	857	99215	59	1519	99215	58575
10	122	949	115725	62	1519	115725	61660
10.5	128	1047	133971	65	1519	133971	64746
11	134	1149	154041	68	1519	154041	67831
11.5	140	1256	176022	71	1519	176022	70917
12	146	1367	200000	74	1519	200000	74002
	Surplus	Parallel	Power	Parallel	Parallel	Power	Parallel
	power	electrolyzer 1	consumed	electrolyzer	electrolyzer 2	consumed	electrolyzer
	of series	allows power	by parallel	1 surplus	allows power	by parallel	2 surplus
Wind	electrolyzers	consumption	electrolyzer	power	consumption	electrolyzer	power
(m/s)	(w)	(w)	1 (w)	(w)	(w)	2 (w)	(w)
4	−17271
4.5	−17216
5	−16378
5.5	−14671
6	−12009
6.5	−8295
7	−3467
7.5	2576	46233	2576	−43657
8	9921	49318	9921	−39397
8.5	18656	52404	18656	−33748
9	28867	55489	28867	−26623
9.5	40641	58575	40641	−17934
10	54065	61660	54065	−7596
10.5	69225	64746	69225	4480	46233	4480	−41753
11	86210	67831	86210	18379	49318	18379	−30940
11.5	105105	70917	105105	34188	52404	34188	−18216
12	125998	74002	125998	51995	58575	51995	−6580

When the effective power of the wind turbine starts cutting in, the DC voltage is 48.8 volts, the basic electrodes are set with 26 series electrodes, the cut-in current is 151.85 amperes, the reference current is set at 0.1 amp/cm², the maximum reference current is set at 0.333 amp/cm², and the electrolyzer is set at 0.333 amp/cm². An electrolyzer with effective size of 151.85/0.1=1519 cm² and electrode with 1519 cm² does not need an additional electrolyzer when the wind speed is not over 7 m/s. In this embodiment, the size of the parallel electrolyzer is the same as that of the basic electrolyzer. One electrolyzer can be connected in parallel when the wind speed is lower than 10.5 m/s. When the wind speed reaches or exceeds 10.5 m/s, the second electrolyzer is required. However, if the parallel electrolytes are set at a current of 534 amp/cm² at a wind speed of 7.5 m/s, the size of the parallel electrolyzer is 534/0.1=5340 cm², and one electrolyzer in parallel can meet the needs of the fluctuating power supply.

Example 5

In Example 5, a doubly-fed 1.5 MW wind turbine is used as the power supply, and 0.055 amp is used as the reference current scheme. Example 5 uses an existing 1500-kilowatt doubly-fed wind turbine as the power source for the electrolyzer. The wind/power characteristics of this type of wind turbine are as follows. Since the doubly-fed wind turbine has the same voltage and frequency in most wind speed ranges, the power. The difference is only in the current as shown in Table 5-1 and results in Table 5-2:

TABLE 5-1
Wind
(m/s)	Vac	Vdc	Idc	Watt

12	110.0	146.3	10253	1500000
11.5	110.0	146.3	9023	1320000
11	110.0	146.3	7897	1155300
10.5	110.0	146.3	6863	1004000
10	110.0	146.3	5926	867000
9.5	110.0	146.3	5079	743000
9	110.0	146.3	4327	633000
8.5	110.0	146.3	3643	533000
8	110.0	146.3	3042	445000
7.5	110.0	146.3	2502	366000
7	110.0	146.3	2030	297000
6.5	110.0	146.3	1627	238000
6	110.0	146.3	1278	187000
5.5	110.0	146.3	984	144000
5	110.0	146.3	738	108000
4.5	110.0	146.3	540	79000
4	110.0	146.3	376	55000

TABLE 5-2
					size of	Power
					electrode	available
				quantity	in basic	for series
Wind	Vdc	Idc	Power	of series	electrolyzer	electrodes
(m/s)	(V)	(A)	(w)	electrodes	(cm2)	(w)
4	146.3	376	55000	74	6835	55000
4.5	146.3	540	79000	74	6835	79000
5	146.3	738	108000	74	6835	108000
5.5	146.3	984	144000	74	6835	144000
6	146.3	1278	187000	74	6835	187000
6.5	146.3	1627	238000	74	6835	238000
7	146.3	2030	297000	74	6835	297000
7.5	146.3	2502	366000	74	6835	366000
8	146.3	3042	445000	74	6835	445000
8.5	146.3	3643	533000	74	6835	533000
9	146.3	4327	633000	74	6835	633000
9.5	146.3	5079	743000	74	6835	743000
10	146.3	5926	867000	74	6835	867000
10.5	146.3	6863	1004000	74	6835	1004000
11	146.3	7897	1155300	74	6835	1155300
11.5	146.3	8887	1300204	74	6835	1300204
12	146.3	10253	1500000	74	6835	1500000
	Max
	allowable
	power			Parallel	Power	Parallel
	consumption	electrolyzer	size of	electrolyzers	consumption	electrolyzer
	of series	surplus	parallel	allow power	by parallel	surplus
Wind	electrodes	power	electrolyzer	consumption	electrolyzer	power
(m/s)	(w)	(w)	(cm2)	(w)	(w)	(w)
4	300000	−245000
4.5	299988	−220988
5	299988	−191988
5.5	299988	−155988
6	299988	−112988
6.5	299988	−61988
7	299988	−2988
7.5	299988	66012	45486	1996364	66012	−1930352
8	299988	145012	45486	1996381	145012	−1851369
8.5	299988	233012	45486	1996381	233012	−1763369
9	299988	333012	45486	1996381	333012	−1663369
9.5	299988	443012	45486	1996381	443012	−1553369
10	299988	567012	45486	1996381	567012	−1429369
10.5	299988	704012	45486	1996381	704012	−1292369
11	299988	855312	45486	1996381	855312	−1141069
11.5	299988	1000216	45486	1996381	1000216	−996165
12	299988	1200012	45486	1996381	1200012	−796369

In Example 5, the reference current is set at 0.055 amp/cm², the maximum reference current is set at 0.3 amp/cm², and the size of the basic electrolytic cell is 376/0.55=6835 cm². When the wind speed reaches 7.5 m/s, an electrolytic cell needs to be connected in parallel, and the size of the parallel electrolytic cell is 2502/0.55=45486 cm². Under the rated power of 12 m/s, one basic electrolytic cell and one parallel electrolytic cell can meet the demand, and there is a surplus of nearly 80 kilowatts, so the size of the parallel electrolyzer can also be appropriately reduced to reduce equipment costs.

Example 6

In Example 6, a 500 kw with 144 volts solar power station is used as the power source, and 0.2 amp is used as the reference current scheme. Example 6 consists of 2000 groups of 250 watts with 24 volts solar panels, which are connected by 4 strings and 500 parallel connecting to form a 144 volt (145 volt)/500 kw solar power station. The reference current is set at 0.2 amp/cm² and the maximum reference current is set at 0.3 amp/cm².

						Max allowable				Max allowable
				size of	available	power			Usable	power
				basic	power for	consumption	Series	size of	power of	consumption	Parallel
			quantity	electro-	series	of series	eectrode	parallel	parallel	of parallel	electrolyzer
			of series	lyzer	electrodes	electrodes	surplus	eectrolyzer	electrolyzers	electrolyzers	surplus
Pdc	Vdc	I dc	electrodes	(cm 2)	(w)	(w)	power (w)	(cm 2)	(w)	(w)	power (w)

40000	40	1000	22	5000	40000	60000	−20000
50625	45	1125	25	5000	50625	67500	−16875
62500	50	1250	28	5000	62500	75000	−12500
75625	55	1375	31	5000	75625	82500	−6875
90000	60	1500	33	5000	90000	90000	0
105625	65	1625	36	5000	105625	97500	8125	8125	8125	158438	−150313
122500	70	1750	39	5000	122500	105000	17500	8125	17500	170625	−153125
140625	75	1875	42	5000	140625	112500	28125	8125	28125	182813	−154688
160000	80	2000	44	5000	160000	120000	40000	8125	40000	195000	−155000
180625	85	2125	47	5000	180625	127500	53125	8125	53125	207188	−154063
202500	90	2250	50	5000	202500	135000	67500	8125	67500	219375	−151875
225625	95	2375	53	5000	225625	142500	83125	8125	83125	231563	−148438
250000	100	2500	56	5000	250000	150000	100000	8125	100000	243750	−143750
275625	105	2625	58	5000	275625	157500	118125	8125	118125	255938	−137813
302500	110	2750	61	5000	302500	165000	137500	8125	137500	268125	−130625
330625	115	2875	64	5000	330625	172500	158125	8125	158125	280313	−122188
360000	120	3000	67	5000	360000	180000	180000	8125	180000	292500	−112500
387500	125	3100	69	5000	387500	187500	200000	8125	200000	304688	−104688
419900	130	3230	72	5000	419900	195000	224900	8125	224900	316875	−91975
452250	135	3350	75	5000	452250	202500	249750	8125	249750	329063	−79313
485800	140	3470	78	5000	485800	210000	275800	8125	275800	341250	−65450
500000	145	3448	81	5000	500000	217500	282500	8125	282500	353438	−70938

Assuming the sunlight is not strong, the starting voltage is 40 volts. The current is 1000 amps, the effective size of the series electrolytic cell is 1000×10000/2000=5000 cm², when the voltage rises to 65 volts, an electrolytic cell needs to be connected in parallel, and the effective size of the electrolytic cell is 1625×10000/2000=8125 amp/cm². After connecting an electrolyzer in parallel, even when the sun turns to the strongest, the electrolyzer still has a surplus capacity of 70 kw, so the actual parallel electrolyzer can appropriately reduce the area to reduce the cost.

Example 7

In Example 7, a 500 kw with 144 volts solar power station is used as the power source, using 0.095 amps as a reference current scheme. Example 7 is a solar power station with the same composition as Example 6. In Example 7, the reference current is set to 0.095 amp/cm², and the maximum reference current is set to 0.3 amp/cm². In Example 7, since the reference current is reduced from 0.2 amp/cm² in Example 6 to 0.095 amp/cm² in Example 7, there is no need to connect an electrolyzer in parallel even when the sun is the strongest, but the basic electrolyzers size is determined by the implementation of the 5000 cm² from Example 6 are increased to 10526 cm² to Example 7. When the sunlight is not strong enough, the equipment utilization ratio of the electrolysis device is low.

					Available	Max allowable	Surplus
				size of	power of	power	power of
				basic	series	consumption	series
			quantity of	electrolyzer	electrodes	of series	electrolyzers
Pdc	Vdc	I dc	electrodes	(cm 2)	(w)	electrodes (w)	(w)

40000	40	1000	22	10526	40000	138947	−98947
50625	45	1125	25	10526	50625	156311	−105686
62500	50	1250	28	10526	62500	173679	−111179
75625	55	1375	31	10526	75625	191047	−115422
90000	60	1500	33	10526	90000	208415	−118415
105625	65	1625	36	10526	105625	225783	−120158
122500	70	1750	39	10526	122500	243151	−120651
140625	75	1875	42	10526	140625	260519	−119894
160000	80	2000	44	10526	160000	277886	−117886
180625	85	2125	47	10526	180625	295254	−114629
202500	90	2250	50	10526	202500	312622	−110122
225625	95	2375	53	10526	225625	329990	−104365
250000	100	2500	56	10526	250000	347358	−97358
275625	105	2625	58	10526	275625	364726	−89101
302500	110	2750	61	10526	302500	382094	−79594
330625	115	2875	64	10526	330625	399462	−68837
360000	120	3000	67	10526	360000	416830	−56830
387500	125	3100	69	10526	387500	434198	−46698
419900	130	3230	72	10526	419900	451565	−31665
452250	135	3350	75	10526	452250	468933	−16683
485800	140	3470	78	10526	485800	486301	−501
500000	144	3448	80	10526	500000	500196	−196

Knowing through the description of above 7 examples, countless combinations can be generated by changing the parameters such as the reference current, the maximum reference current, the cut-in voltage, the ratio of the minimum cut-in current and the reference current etc. to form new and different types of electrolyzers combinations. However, no matter the basic electrolyzer or the parallel electrolyzer, they are composed of a series of identical basic electrodes plus controllable series electrodes. At the same time, it can be clearly understood from above 7 typical embodiments that the present invention is a fusion innovative invention under the condition of fully understanding the characteristics of wind energy, solar power and electrolysis with very large energy fluctuations, and should be granted a patent.

The invention discloses a structure and control method of an electrode and an electrolytic cell which independently utilize clean energy with a very large power fluctuation range as an electrolysis power source, can be used for hydrogen production, oxygen production, etc. Technically, the initial number of electrodes is determined by the minimum cut-in voltage value of fluctuating power sources, such as wind or solar power. When the voltage increases, more electrodes are added in to maintain each electrode to remain at a stable 2-volt level. Due to unstable power sources, the ratio of the minimum cut-in current and the reference current corresponding to the lowest cut-in voltage value determine the effective number of the electrodes. When the voltage and current of the fluctuating power supply increase within a certain range, more series electrodes are connected to the basic electrolyzer. When the power supply voltage and current continue to increase and exceed the carrying range of the electrolyzer, additional electrolyzers with the same number of electrodes in series are automatically connected into the electrolyzer in parallel. On the contrary, a number of series electrodes or even parallel electrolyzers could be cut out when the voltage and current of the power source drop, in order to achieve more efficient electrolysis that uses large power and current fluctuation power source.

The above descriptions are only some representative examples of the present invention, and all changes and combinations of electrodes and electrolytic cells made according to the patent application method of the present invention shall fall within the scope of the present invention.